Method for preparing ethylene copolymer
Abstract
A process for preparing an ethylene copolymer in the presence of free-radical polymerization initiator at pressures from 150 MPa to 350 MPa and temperatures from 100° C. to 350° C., by copolymerizing ethylene and a comonomer having a C≡C bond and optionally further comonomers, wherein the comonomer having the C≡C bond is represented by formula wherein R 1 is hydrogen or methyl; X 1 is —CO—O— or —CO—NH—; R 2 is —CH 2 —O—, —O—CO—, —Si(CH 3 ) 2 —, —Si(CH 3 ) 2 —O— or —CR 5 R 6 — wherein R 5 and R 6 are independently selected from hydrogen, methyl, ethyl and hydroxyl; n is an integer from 1 to 32 and R 2 is same or different from each other when n is 2 to 32 ; and R 3 is —C≡C— and R 4 is hydrogen, C 1 -C 10 linear or branched alkyl, C 1 -C 10 linear or branched hydroxyalkyl or phenyl, or the unit R 3 -R 4 stands for wherein X 2 is F, Cl, Br or I.
Claims
exact text as granted — not AI-modifiedThe invention claimed is:
1. A process for preparing an ethylene copolymer in the presence of free-radical polymerization initiator at pressures in the range of from 150 MPa to 350 MPa and temperatures in the range of from 100° C. to 350° C. by copolymerizing ethylene and a comonomer having a C≡C bond and optionally further comonomers, wherein the comonomer having the C≡C bond is represented by formula
wherein
R 1 is hydrogen or methyl;
X 1 is —CO—O— or —CO—NH—;
R 2 is —CH 2 —O—, —O—CO—, —Si(CH 3 ) 2 —, —Si(CH 3 ) 2 —O— or —CR 5 R 6 — wherein R 5 and R 6 are independently selected from hydrogen, methyl, ethyl and hydroxyl;
n is an integer from 1 to 32 and R 2 is same or different from each other when n is 2 to 32; and
R 3 is —C≡C— and R 4 is hydrogen, C 1 -C 10 linear or branched alkyl, C 1 -C 10 linear or branched hydroxyalkyl or phenyl, or the unit R 3 -R 4 stands for
wherein X 2 is F, Cl, Br or I, and
wherein the copolymerization is performed in the presence of a chain transfer agent selected from the group consisting of propionaldehyde, n-heptane, propylene, propane, isopropanol and acetone.
2. The process according to claim 1 , wherein the comonomer having the C≡C bond is compound (I) wherein X 1 is —CO—O—, R 2 is —CH 2 —, n is from 1 to 22, and R 3 is —C≡C—and R 4 is methyl or hydrogen or R 3 -R 4 stands for
3. The process according to claim 1 , wherein the comonomer having the C≡C bond is selected from the group consisting of propargyl acrylate, propargyl methacrylate and 2- methyl-acrylic acid 3-(cyclooct-2-ynyloxy)-propyl ester.
4. The process according to claim 1 , wherein the comonomer having the C≡C bond is propargyl methacrylate or propargyl acrylate.
5. The process according to claim 4 , wherein the copolymerization is performed at temperatures of 150° C. to 210° C. and at pressures from 160 MPa and 250 MPa.
6. The process according to claim 1 , wherein the amount of the comonomer having the C≡C bond is 0.1-10 mol % of the total weight of ethylene and all comonomers.
7. The ethylene copolymer obtained by the process of claim 1 .
8. The ethylene copolymer according to claim 7 , wherein the ethylene copolymer has a number average molecular weight M n of at least 5.0 kg/mol and/or a weight average molecular weight M w of at least 50 kg/mol.
9. An article comprising the ethylene copolymer according to claim 7 .
10. The article according to claim 9 , wherein the article is a film or sheet.
11. The article according to claim 10 , wherein the film is or is a component of food packaging , consumer durable packaging, disposable diapers, textiles, agricultural film, shrink film, medical packaging, cable insulations, mulching film, protective film, or polymer coatings.
12. The article according to claim 11 , wherein the film or sheet has a thickness of 5 to 500 micrometers.
13. The article according to claim 9 , wherein the article is an injection moulded article, a blow moulded article, a sheet vacuum formed article, or a polymer coating.
14. The article according to claim 13 , wherein the article is a container, bottle, rigid packaging, pail, or tray.
15. A process for preparing an ethylene copolymer in the presence of free-radical polymerization initiator at pressures in the range of from 150 MPa to 350 MPa and temperatures in the range of from 100° C. to 350° C. by copolymerizing ethylene and a comonomer having a C≡C bond and optionally further comonomers, wherein the comonomer having the C≡C bond is represented by formula
wherein
R 1 is hydrogen or methyl;
X 1 is —CO—O— or —CO—NH—;
R 2 is —CH 2 —O—, —O—CO—, —Si(CH 3 ) 2 —, —Si(CH 3 ) 2 —O— or —CR 5 R 6 — wherein R 5 and R 6 are independently selected from hydrogen, methyl, ethyl and hydroxyl;
n is an integer from 1 to 32 and R 2 is same or different from each other when n is 2 to 32; and
R 3 is —C≡C— and R 4 is hydrogen, C 1 -C 10 linear or branched alkyl, C 1 -C 10 linear or branched hydroxyalkyl or phenyl, or the unit R 3 -R 4 stands for
wherein X 2 is F, Cl, Br or I, and
wherein the process is performed in a tubular reactor.
16. A process for preparing an ethylene copolymer in the presence of free-radical polymerization initiator at pressures in the range of from 150 MPa to 350 MPa and temperatures in the range of from 100° C. to 350° C. by copolymerizing ethylene and a comonomer having a C≡C bond and optionally further comonomers, wherein the comonomer having the C≡C bond is represented by formula
wherein
R 1 is hydrogen or methyl;
X 1 is —CO—O—;
R 2 is —CH 2 —;
n is an integer from 1 to 22; and
R 3 is —C≡C— and R 4 is methyl or hydrogen or R 3 -R 4 stands for
17. The process according to claim 16 , wherein the copolymerization is performed in the presence of a chain transfer agent selected from the group consisting of propionaldehyde, n-heptane, propylene, propane, isopropanol and acetone.Cited by (0)
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